Temperature control apparatus, processing apparatus, and temperature control method

ABSTRACT

A temperature control apparatus ( 70 ) includes a heat exchanger ( 71 ) configured to exchange heat with the surroundings using a phase change of a refrigerant, a rotary pump ( 73 ) configured to receive the refrigerant from the heat exchanger ( 71 ) and fuse the refrigerant with oil contained inside the rotary pump, and an oil water separator ( 74 ) configured to receive the refrigerant fused with the oil from the rotary pump ( 73 ) and separate the refrigerant from the oil. The temperature control apparatus further includes a refrigeration cycle that implements a cooling function by circulating the refrigerant separated from the oil back to the heat exchanger ( 71 ).

TECHNICAL FIELD

The present invention relates to a temperature control apparatus, aprocessing apparatus, and a temperature control method.

BACKGROUND ART

Temperature control apparatuses are known that circulate a refrigerantto cool or heat an object using vaporization heat absorbed from thesurroundings and condensation heat released to the surroundings as aresult of a phase change in the refrigerant. For example, PatentDocument 1 discloses a temperature control apparatus that uses thevaporization heat of a refrigerant to cool an electrostatic chuckarranged within a plasma reactor.

PRIOR ART DOCUMENTS Patent Documents

Patent Document 1: Japanese Laid-Open Patent Publication No. 2007-116098

SUMMARY OF THE INVENTION Problem to be Solved by the Invention

However, a gas that destroys the ozone layer is used in the refrigerantcirculated within the temperature control apparatus disclosed in PatentDocument 1. Hydrocarbon-based gases are examples of ozone depletingsubstances that destroy the ozone layer, and waste refrigerantcontaining such substance is harmful to the environment in that itcauses global warming.

The refrigeration cycle of the temperature control apparatus disclosedin Patent Document 1 includes a heat exchanger, a compressor, acondenser, and an expansion valve. In the structure disclosed in PatentDocument 1, a refrigerant, which is inherently gaseous, is liquefied andis converted back to gas within a heat exchanger arranged inside amounting table. Accordingly, the phase change between gas and liquid hasto be controlled under high pressure. Thus, for example, in therefrigeration cycle disclosed in Patent Document 1, the interior of acirculation cycle has to be designed to withstand a high pressure ofapproximately 15-20 atm. Accordingly, in Patent Document 1, a highlydurable pressure chamber has to be provided by arranging a thick wallaround the heat exchanger, for example, so that the heat exchanger maybe prevented from deforming even under a high pressure. As a result, theheat capacity of the heat exchanger is increased to thereby degradetemperature responsiveness.

In light of the above, one aspect of the present invention relates toproviding a temperature control apparatus, a processing apparatus, and atemperature control method that enable temperature control without usingan ozone depleting substance in the refrigerant.

Means for Solving the Problem

According to one embodiment of the present invention, a temperaturecontrol apparatus is provided that includes a heat exchanger configuredto exchange heat using a phase change of a refrigerant, a rotary pumpconfigured to receive the refrigerant from the heat exchanger and fusethe refrigerant with oil contained inside the rotary pump, and an oilrefrigerant separator configured to receive the refrigerant fused withthe oil from the rotary pump and separate the refrigerant from the oil.The temperature control apparatus further includes a refrigeration cyclethat implements a cooling function by circulating the refrigerantseparated from the oil back to the heat exchanger.

According to another embodiment of the present invention, a plasmaprocessing apparatus is provided that includes a processing chamber inwhich a plasma process is performed; a gas supply source configured tosupply gas to the processing chamber; a plasma source configured tosupply power for plasma generation and generate plasma from gas withinthe processing chamber; a heat exchanger that is arranged in at leastone of the processing chamber, a mounting table arranged in theprocessing chamber, an upper electrode arranged in the processingchamber, and a deposition shield arranged in the processing chamber, andis configured to exchange heat using a phase change of a refrigerant; arotary pump configured to receive the refrigerant from the heatexchanger and fuse the refrigerant with oil contained inside the rotarypump; and an oil refrigerant separator configured to receive therefrigerant fused with the oil from the rotary pump and separate therefrigerant from the oil. The plasma processing apparatus furtherincludes a refrigeration cycle that implements a cooling function bycirculating the refrigerant separated from the oil back to the heatexchanger.

According to another embodiment of the present invention, a processingapparatus is provided that includes a temperature control apparatus thatis mounted to a temperature control object and is configured to controla temperature of the temperature control object. The temperature controlapparatus includes a heat exchanger configured to exchange heat using aphase change of a refrigerant; a rotary pump configured to receive therefrigerant from the heat exchanger and fuse the refrigerant with oilcontained inside the rotary pump; and an oil refrigerant separatorconfigured to receive the refrigerant fused with the oil from the rotarypump and separate the refrigerant from the oil. The temperature controlapparatus further includes a refrigeration cycle that implements acooling function by circulating the refrigerant separated from the oilback to the heat exchanger.

According to another embodiment of the present invention, a temperaturecontrol method is provided that is implemented by a temperature controlapparatus including a heat exchanger configured to exchange heat using aphase change of a refrigerant, a rotary pump configured to receive therefrigerant from the heat exchanger and fuse the refrigerant with oilcontained inside the rotary pump, and an oil refrigerant separatorconfigured to receive the refrigerant fused with the oil from the rotarypump and separate the refrigerant from the oil. The temperature controlmethod includes the steps of circulating the refrigerant separated fromthe oil back to the heat exchanger; and adjusting at least one of arotation speed of a rotor of the rotary pump, a position of a valvearranged at a connecting portion of the rotary pump and the heatexchanger, and a position of an airflow adjustment valve arranged at aconnecting portion of the oil refrigerant separator and the heatexchanger.

Advantageous Effect of the Invention

According to an aspect of the present invention, a temperature controlapparatus, a processing apparatus, and a temperature control method maybe provided that enable temperature control without using an ozonedepleting substance in the refrigerant.

BRIEF DESCRIPTION OF THE DRAWINGS

FIG. 1 illustrates an overall configuration of a plasma processingapparatus that uses a temperature control apparatus according to a firstembodiment of the present invention;

FIG. 2 illustrates an overall configuration of the temperature controlapparatus according to the first embodiment;

FIG. 3 illustrates a heat exchanger of the temperature control apparatusaccording to the first embodiment;

FIG. 4 is a flowchart illustrating operations of the temperature controlapparatus according to the first embodiment;

FIG. 5 is a time chart illustrating operations of the temperaturecontrol apparatus according to the first embodiment;

FIG. 6 is a flowchart illustrating operations of the temperature controlapparatus according to the first embodiment;

FIG. 7 illustrates an overall configuration of a temperature controlapparatus according to a second embodiment of the present invention;

FIG. 8 illustrates an operating state of the temperature controlapparatus according to the second embodiment during operation of arefrigeration cycle;

FIG. 9 illustrates an operating state of the heat exchanger duringoperation of the refrigeration cycle of the temperature controlapparatus according to the second embodiment;

FIG. 10 illustrates an operating state of the temperature controlapparatus according to the second embodiment during operation of aheating cycle;

FIG. 11 illustrates the heat exchanger during operation of the heatingcycle of the temperature control apparatus according to the secondembodiment; and

FIG. 12 illustrates the heat exchanger during operation of theheating/refrigeration cycle of the temperature control apparatusaccording to the second embodiment.

EMBODIMENTS FOR IMPLEMENTING THE INVENTION

In the following, embodiments of the present invention are describedwith reference to the accompanying drawings. Note that elements havingsubstantially the same functions or features may be given the samereference numerals and overlapping descriptions thereof may be omitted.

<Introduction>

In an ordinary refrigeration cycle, an ozone depleting gas such ashydrocarbon-based gas is used in a refrigerant that is circulated withina temperature control apparatus. Refrigerant waste containing such asubstance is harmful to the environment in that it causes globalwarming. In view of the above, embodiments described below relate to atemperature control apparatus that is capable of performing temperaturecontrol without using such ozone depleting substance. In the embodimentsdescribed below, water is used as the refrigerant and vaporization heatof water is used for cooling. In this way, a temperature controlapparatus may be provided that uses vaporization heat absorbed from thesurroundings or condensation heat released to the surroundings as aresult of a phase change in water to cool or heat an object.

Also, in the temperature control apparatus according to embodiments ofthe present invention, the interior of a heat exchanger does not have tobe set to a high pressure. In fact, the pressure within the heatexchanger has to be reduced in order to enable vaporization of a liquidunder a temperature of less than 100° C. Thus, in a case where thetemperature control apparatus according to an embodiment of the presentinvention is implemented in a plasma processing apparatus, apredetermined portion of the temperature control apparatus may be easilycontrolled to a reduced-pressure in view of the fact that controllingthe pressure of a chamber to a reduced-pressure atmosphere is normallyperformed in the plasma processing apparatus. Also, in embodiments ofthe present invention, a chamber having a small heat capacity may beused in the heat exchanger, and in this way, temperature responsivenessmay be improved and energy resources may be conserved.

As described below, in the temperature control apparatus according toembodiments of the present invention, accurate temperature control maybe performed without using an ozone depleting substance in therefrigerant.

First Embodiment

[Overall Configuration of Plasma Processing Apparatus using TemperatureControl Apparatus]

First, an overall configuration of a plasma processing apparatus thatuses a temperature control apparatus according to a first embodiment ofthe present invention is described with reference to FIG. 1.

The plasma processing apparatus 1 illustrated in FIG. 1 is configured asa RIE (Reactive Ion Etching) plasma processing apparatus. The plasmaprocessing apparatus 1 includes a cylindrical chamber (processingchamber 10) made of a metal such as aluminum or stainless steel, forexample. The processing chamber 10 is grounded.

A mounting table 12 configured to hold a semiconductor wafer W(hereinafter, simply referred to as a “wafer W”) thereon as a workpieceis arranged within the processing chamber 10. In such a state,microfabrication processes such as etching may be performed on the waferW using the action of plasma. The mounting table 12 may be made ofaluminum, for example, and is supported on a cylindrical support 16 viaan insulating cylindrical holder 14. The cylindrical support 16 extendsvertically upward from a bottom of the processing chamber 10. A focusring 18 that may be made of quartz, for example, is disposed on a topsurface of the cylindrical holder 14 to surround a top surface edge ofthe mounting table 12.

An exhaust path 20 is formed between a sidewall of the processingchamber 10 and the cylindrical support 16. A ring-shaped baffle plate 22is arranged in the exhaust path 20. An exhaust port 24 is formed at abottom portion of the exhaust path 20 and is connected to an exhaustdevice 28 via an exhaust line 26. The exhaust device 28 includes avacuum pump (not shown) and is configured to depressurize a processingspace within the processing chamber 10 to a predetermined vacuum level.A gate valve 30 configured to open/close an entry/exit port for thewafer W is provided at the sidewall of the processing chamber 10.

A high frequency power supply 32 for plasma generation is electricallyconnected to the mounting table 12 via a matching unit 34 and a powerfeed rod 36. The high frequency power supply 32 is configured to apply ahigh frequency power of 60 MHz, for example, to the mounting table 12.In this way, the mounting table 12 also acts as a lower electrode.Further, a shower head 38, which is described below, is provided at aceiling portion of the processing chamber 10. The shower head 38 acts asan upper electrode of a ground potential. In this way, a high frequencyvoltage from the high frequency power supply 32 is capacitativelyapplied between the mounting table 12 and the shower head 38. The highfrequency power supply 32 is an example of a plasma source that suppliespower for plasma generation to the processing chamber 10 and generatesplasma from gas within the processing chamber 10.

An electrostatic chuck 40 configured to hold the wafer W by anelectrostatic attractive force is provided on the top surface of themounting table 12. The electrostatic chuck 40 includes an electrode 40 athat is made of a conductive film and is arranged between a pair ofinsulating films 40 b and 40 c. A DC power supply 42 is electricallyconnected to the electrode 40 a via a switch 43. The electrostatic chuck40 electrostatically attracts and holds the wafer W by a Coulomb forcegenerated by a DC voltage from the DC power supply 42.

The electrostatic chuck 40 is cooled by a temperature control unit 70.The temperature control unit 70 includes a heat exchanger 71, a rotarypump 73, and an oil water separator 74. The heat exchanger 71 isarranged inside the mounting table 12. The heat exchanger 71 isconnected to the rotary pump 73 and the oil water separator 74 via asuction pipe 72. The heat exchanger 71 is also connected to the oilwater separator 74 via a water pipe 75. A valve 76 is arranged at thesuction pipe 72 between the heat exchanger 71 and the rotary pump 73. Anairflow adjustment valve 77 is arranged at the water pipe 75 between theheat exchanger 71 and the oil water separator 74. The mounting table 12may be cooled by supplying a refrigerant to the temperature controlapparatus 70 having the above configuration. Note that detailedfunctions and operations of the temperature control apparatus 70 aredescribed below.

A heat transfer gas supply source 52 is configured to supply a heattransfer gas such as He gas between a top surface of the electrostaticchuck 40 and a rear surface of the wafer W through a gas supply line 54.

The shower head 38 disposed at the ceiling portion of the processingchamber 10 includes an electrode plate 56 having multiple gas holes 56 aand an electrode supporting body 58 configured to detachably hold theelectrode plate 56. A buffer chamber 60 is formed within the electrodesupporting body 58. A gas inlet 60 a of the buffer chamber 60 isconnected to a gas supply line 64, which is connected to a gas supplysource 62. In this way, desired gas may be supplied to the processingchamber 10 from the gas supply source 62.

A magnet 66 is arranged to extend annularly or concentrically around theprocessing chamber 10. An RF electric field is formed in a plasmagenerating space between the shower head 38 and the mounting table 12within the processing chamber 10 along a vertical direction by the highfrequency power supply 32. Due to a high frequency discharge,high-density plasma may be generated around the surface of the mountingtable 12.

A controller 68 is configured to control the individual components ofthe plasma processing apparatus 1 such as the exhaust device 28, thehigh frequency power supply 32, a switch 43 for the electrostatic chuck40, the matching unit 34, the heat transfer gas supply source 52, thegas supply source 62, and the airflow adjustment valve 77. Thecontroller 68 may also be connected to a host computer (not shown), forexample. The controller 80 includes a CPU (Central Processing Unit), aROM (Read Only Memory) and a RAM (Random Access Memory), which are notshown. The CPU executes a process according to a recipe stored in astorage unit. In this way, an etching process may be controlled by theCPU. The storage unit may be configured as the ROM or the RAM using asemiconductor memory, a magnetic disk, or an optical disk, for example.The recipe may be stored in a storage medium and loaded in the storageunit via a driver (not shown), for example. Alternatively, the recipesmay be downloaded from a network (not shown) and stored in the storageunit. Also, in some embodiments, a DSP (Digital Signal Processor) may beused instead of the CPU to implement the above-described functions ofvarious components of the plasma processing apparatus 1. Note thatfunctions of the controller 68 may be implemented by software orhardware.

When performing an etching process using the plasma processing apparatus1 having the above-described configuration, first, the gate valve 30 isopened, and the wafer W is loaded into the processing chamber 10 andplaced on the electrostatic chuck 40. Then, an etching gas is introducedinto the processing chamber 10 from the gas supply source 62 at apredetermined flow rate and a predetermined flow rate ratio, and theinternal pressure of the processing chamber 10 is reduced to apredetermined pressure by the exhaust device 28. Further, a highfrequency power of a certain power level is applied to the mountingtable 12 from the high frequency power supply 32. Also, a DC voltagefrom the DC power supply 42 is applied to the electrode 40 a of theelectrostatic chuck 40 so that the wafer W may be fixed to theelectrostatic chuck 40. The etching gas sprayed into the processingchamber 10 from the shower head 38 is decomposed by the high frequencypower from the high frequency power supply 32, and as a result, plasmais generated within a plasma generating space between the upperelectrode (shower head 38) and the lower electrode (mounting table 12).A main surface of the wafer W is etched by radicals and ions containedin the generated plasma.

Temperature control of the wafer W is important in performing preciseand accurate microfabrication such as etching on the wafer W.Accordingly, as illustrated in FIG. 1, the heat exchanger 71 is arrangedinside the mounting table 12, which is arranged near the electrostaticchuck 40, and the heat exchanger 71 is configured to cool theelectrostatic chuck 40 and the mounting table 12. In the following,configurations and operations of the temperature control apparatus 70including the heat exchanger 71 are described.

[Temperature Control Apparatus]

FIG. 2 illustrates an overall configuration of the temperature controlapparatus 70. The temperature control apparatus 70 includes the heatexchanger 71, the rotary pump 73, and the oil water separator 74. Theheat exchanger 71 and the rotary pump 73 are interconnected via thesuction pipe 72. The valve 76 is arranged at the suction pipe 72. Theheat exchanger 71 and the oil water separator 74 are interconnected viathe water pipe 75. The airflow adjustment valve 77 is arranged at a pipebranching out from the water pipe 75. The airflow adjustment valve 77 isconfigured to adjust the amount of air to be introduced into water thatis circulated within the water pipe 51. The rotary pump 73 and the oilwater separator 74 are interconnected by reciprocating pipes 78 forcirculating oil. By circulating water through the temperature controlapparatus 70 that is arranged into a tubular structure as describedabove, the temperature control apparatus 70 may function as arefrigeration cycle for cooling the surroundings of the heat exchanger71.

(Heat Exchanger)

The heat exchanger 71 is configured to exchange heat with itssurrounding in response to a phase change in water. The heat exchangefunction of the heat exchanger 71 is described below with reference toFIG. 3. Like a typical refrigeration cycle, the heat exchanger 71includes an evaporation chamber 71 a as an indoor unit. The heatexchanger 71 has functions of cooling and converting external hot airinto cool air, and removing heat from an object located near the heatexchanger 71 to lower the temperature of the object, for example. Watercirculated within the water pipe 75 is introduced into the evaporationchamber 71 a. The heat exchanger 71 vaporizes the water inside theevaporation chamber 71 a, which his controlled to a reduced-pressureatmosphere, to generate water vapor. The generated water vapor isdischarged toward the suction pipe 72. In this way, the heat exchanger71 cools the surroundings of the heat exchanger 71 using vaporizationheat absorbed from the exterior when the phase of water changes fromliquid to gas (water vapor).

To cause evaporation of water at a temperature below 100° C.corresponding to the boiling point of water under normal pressure, theinterior of the evaporation chamber 71 a has to be controlled to areduced-pressure atmosphere (vacuum). In the present embodiment and inthe second embodiment described below, the rotary pump 73 (oil pump) asillustrated in FIG. 2 is used to control the interior of the evaporationchamber 71 a to a reduced-pressure atmosphere. In the evaporationchamber 71 a that is controlled to a reduced-pressure atmosphere byoperating the rotary pump 73, water is turned into water vapor (reducedpressure water vapor) and is diffused within the evaporation chamber 71a.

(Rotary Pump)

As illustrated in FIG. 2, the rotary pump 73 includes a rotor 73 a. Therotor 73 a is rotated by the power of a motor (not shown). In FIG. 2, aninlet 73 c for introducing water vapor is arranged at an upper rightside portion of the rotary pump 73, and an exhaust port 73 b fordischarging air is arranged at an upper left side portion of the rotarypump 73. In the rotary pump 73, the rotor 73 a is rotated to dischargeair outside the apparatus via the exhaust port 73 b. An oil layer isprovided at a bottom portion within the rotary pump 73. The oil layeracts as a sealing material for separating the internal space of therotary pump 73 into a right side space and a left side space. In thisway, the internal space of the rotary pump 73 is divided into two (rightchamber and left chamber in FIG. 2). The rotary pump 73 controls theright chamber to be in a reduced-pressure state by rotating the rotor 73a clockwise as illustrated in FIG. 2. In this way, the right chamber mayconstitute a reduced-pressure space and the left chamber may constitutean atmospheric pressure space. The reduced-pressure space of the rotarypump 73 is connected to the evaporation chamber 71 a. By arranging theright side space of the rotary pump 73 to constitute a reduced-pressurespace, the internal space of the evaporation chamber 71 a may becontrolled to a reduced-pressure space.

The rotary pump 73 introduces the reduced-pressure water vapor generatedwithin the evaporation chamber 71 a into its interior, and rotates therotor 73 a to compress the water vapor and fuse the water vapor with theoil inside the rotary pump 73. In the illustrated example of FIG. 2, thereduced-pressure water vapor is represented by a water layer that isseparate from the oil layer within the rotary pump 73. The water vaporintroduced into the rotary pump 73 dissolves into oil. The water vaporthat dissolves into the oil may be handled as liquid water. Accordingly,the mixture of water dissolved into oil is passed through a filter 74 aof the oil water separator 74 and the water is separated from the oil bythe oil water separator 74. In this way, the refrigerant that has beengasified into water vapor at the heat exchanger 71 may be converted backto liquid water using the rotary pump 73 and the oil water separator 74.

(Oil Water Separator)

The water that has been separated from the oil by the oil waterseparator 74 is returned to the water pipe 75 to be reused as therefrigerant. The water is thus recirculated through the water pipe 75,the heat exchanger 71, the suction pipe 72, the rotary pump 73, and theoil water separator 74. The circulated water undergoes a phase changefrom water to water vapor once again at the heat exchanger 71. In thisway, an object near the heat exchanger 71 may be cooled, for example.

The oil separated from the water by the oil water separator 74 isrecovered by the rotary pump 73 via the pipe 78. Note that the oil waterseparator 74 is an example of an oil refrigerant separator that isconfigured to receive the refrigerant fused with oil from the rotarypump 73 and separate the refrigerant from the oil. Also, note that therefrigerant is not limited to water, but may be some other type ofliquid that can be separated from oil. For example, alcohol or ammoniummay be used as the refrigerant instead of water. However, because thelatent heat of water is greater than that of the above exemplaryalternative refrigerants, a greater cooling effect may be achieved byusing water as the refrigerant.

(Refrigeration Cycle)

The circulation cycle as described above may act as a refrigerationcycle. That is, water corresponding to the refrigerant circulatesthrough the heat exchanger 71 (evaporation chamber 71 a), the suctionpipe 72, the rotary pump 73, the oil water separator 74, the water pipe75, and back to the heat exchanger 71 (evaporation chamber 71 a). Byreducing the pressure within the evaporation chamber 71 a, water mayevaporate even under a temperature below 100° C. (e.g. roomtemperature), for example. Accordingly, a phase change from water towater vapor may be prompted at the heat exchanger 71 under a temperatureof 50° C., for example. In the temperature control apparatus 70according to the present embodiment, the surroundings of the heatexchanger 71 may be cooled by removing (absorbing) the vaporization heatfrom the surroundings when the phase change from water to vapor occurs.

[Temperature Control Method]

In the following, a temperature control method for controlling thetemperature of the electrostatic chuck 40 (wafer W) using thetemperature control apparatus 70 according to the present embodiment isdescribed. In the temperature control apparatus 70 according to thepresent embodiment, the temperature of the electrostatic chuck 40 may becontrolled by controlling the flow rate of water being circulated andthe pressure within the evaporation chamber 71 a. Such controloperations may be implemented based on a relevant command from thecontroller 68.

The flow rate of water determines the cooling capacity of therefrigeration cycle. That is, the amount of calories that may be usedfor cooling is proportional to the volume of water that is flown pertime unit. Thus, the flow rate of water may be controlled based on theheat load (kW) that has to be cooled. Accordingly, in the presentembodiment, the controller 68 controls the flow rate of water accordingto an expected heat input from plasma. On the other hand, the pressurewithin the evaporation chamber 71 a may be controlled based on thedesired temperature (° C.) of the heat exchanger 71. For example, in acase where a cooling capacity for cooling a heat load of 1 kW isdesired, the flow rate of water may be unambiguously determined.However, the pressure level to which the evaporation chamber 71 a is tobe adjusted may vary depending on whether the desired temperature of theheat exchanger 71 is 5° C. or 50° C., for example. The controller 68controls the pressure within the evaporation chamber 71 a such that thepressure may be lower in the case where the desired temperature of theheat exchanger 71 is 5° C. compared to the case where the desiredtemperature of the heat exchanger 71 is 50° C.

Note that the controller 68 implements at least one of the followingcontrol methods (1)-(3) upon controlling the pressure within theevaporation chamber 71 a.

(1) Change capacity of rotary pump 73 itself.

(2) Change amount of air introduced into rotary pump 73.

(3) Change amount of air introduced into heat exchanger 71.

In the case of implementing control method (1) that involves changingthe capacity of the rotary pump 73 itself, the power from the motor (notshown) is adjusted to change the rotation speed of the rotor 73 a. Also,in some embodiments, the pressure within the evaporation chamber 71 amay be controlled by increasing or decreasing the number of rotary pumpsthat are operated in a case where a plurality of rotary pumps arearranged in parallel. In the case of implementing control method (2)that involves changing the amount of air introduced into the rotary pump73, the position of the valve 76 may be adjusted to change theconductance of the suction pipe 72. In the case of implementing controlmethod (3) that involves changing the amount of air introduced into heatexchanger 71, the position of the airflow adjustment valve 77 may beadjusted to change the amount of external air introduced into the heatexchanger 71.

As described above, the controller 68 is configured to control thetemperature control operations of the temperature control apparatus 70by controlling at least one of the rotation speed of the rotor 73 a, theposition of the valve 76, and the position of the airflow adjustmentvalve 77. The motor driving the rotor 73 a, the valve 76, and theairflow adjustment valve 77 are connected to the controller 68 and areconfigured to operate based on a command from the controller 68. Atemperature sensor (not shown) is attached to the heat exchanger 71, andthe controller 68 feedback controls the detection result of thetemperature sensor to adjust the pressure within the evaporator 71 a.

[Temperature Control Apparatus Operations]

In the following, operations of the temperature control apparatus 70according to the present embodiment are described with reference to theflowchart of FIG. 4 illustrating a temperature control process.

When the temperature control process of FIG. 4 is started, thecontroller 68 determines whether plasma is turned ON (step S42). Thecontroller 68 may determine that the plasma is turned ON when gas issupplied to the processing chamber 10 and a high frequency power isapplied to the mounting table 12, for example. Alternatively, thecontroller 68 may monitor the temperature of the mounting table 12 usingthe temperature sensor and determine that the plasma is turned ON basedon the detected temperature change of the mounting table 12, forexample. Upon determining that the plasma is turned ON, the controller68 starts operation of the rotary pump 73 and circulates water withinthe temperature control apparatus 70 at a predetermined flow raterequired for cooling according to the heat input from plasma (step S44).

For example, as illustrated in the time chart of FIG. 5, in a case wherethe temperature T of the mounting table 12 is desirably controlled to25° C., and the temperature of the mounting table 12 before starting thepresent process is 25° C., the temperature control apparatus 70 does nothave to perform any temperature control operation. Accordingly, duringthe period from time t0 to time t1 before plasma is turned ON, thecontroller 68 does not circulate water within the temperature controlapparatus 70. Thus, the flow rate MO of water circulated during thisperiod is 0 (zero).

During a period in which plasma is generated through plasma ignition,i.e., while plasma is turned ON, unless some cooling measure isimplemented, the temperature of the mounting table 12 will be raised bythe heat input from plasma and the temperature of the wafer W will bechanged to thereby cause adverse effects on the etching process.Accordingly, once the plasma is turned ON, the refrigeration cycle hasto be promptly driven. For example, during the period from time t1 totime t2 in which plasma is turned ON, if the heat input from plasma is 1kW, a cooling capacity for cooling a heat load of 1 kW is required. Inthis case, the controller 68 starts circulating water at the flow raterequired for cooling 1 kW (approximately 0.0241/min) at the time theplasma is turned ON (steps S42 and S44). In this way, the heat inputfrom plasma may be consumed upon evaporating the water, and thetemperature of the mounting table 12 may be prevented from increasing.

Also, the controller 68 implements at least one of the above controlmethods of (1) rotor 73 a rotation speed control, (2) valve 76 positioncontrol, and (3) airflow adjustment valve 77 position control to adjustthe pressure within the evaporation chamber 71 a and thereby control thetemperature of the heat exchanger 71 to a desired temperature (stepS46). In this way, while plasma is turned ON, the controller 68 feedbackcontrols the pressure within the evaporation chamber 71 a so that thetemperature of the heat exchanger 71 may be controlled to the desiredtemperature. In the example illustrated in FIG. 5, the controller 68reduces the pressure P within the evaporation chamber 71 a from pressurePO (0.1 MPa) to pressure PA (0.001 MPa) to control and maintain thetemperature of the heat exchanger 71 at the desired temperature of 25°C.

Then, the controller 68 determines whether the plasma has been turnedOFF (step S48). The controller 68 repeats the processes of steps S44,S46, and S48 until the plasma is turned OFF. The controller 68 maydetermine that the plasma has been turned OFF when the supply of gas tothe processing chamber 10 and the application of the high frequencypower to the mounting table 12 are terminated, for example.Alternatively, the controller 68 may monitor the temperature of themounting table 12 using the temperature sensor and determine whether theplasma has been turned OFF based on the detected temperature change ofthe mounting table 12, for example. Upon determining that the plasma hasbeen turned OFF, the controller 68 stops the operation of the rotarypump 73 and terminates the circulation of water (step S50). Then, thecontroller 68 increases the pressure within the evaporation chamber 71 ato a pressure level that would not enable water to evaporate within theevaporation chamber 71 a (step S52). In this way, evaporation of watermay be promptly disabled, and as a result, the cooling operation may bepromptly terminated as soon as the plasma is turned OFF.

For example, in FIG. 5, when the plasma is turned OFF at time t2, thecontroller 68 controls the water flow rate Mb to be 0 and controls thepressure P within the evaporation chamber 71 a to an ordinary pressurePB (0.1 MPa). In this way, the cooling operation for cooling theelectrostatic chuck 40 may be promptly terminated, and the temperatureof the mounting table 12 may be prevented from decreasing.

Also, as illustrated in FIG. 5, in a case where a process is started attime t3 and the heat input from plasma in this process is only half theheat input from plasma during the process performed from time t1 to timet2, the controller 68 circulates water at a flow rate Mc that is lowerthan the flow rate Ma of the previous process and adjusts the pressure Pwithin the evaporation chamber 71 a to a pressure PC that is higher thanthe pressure PA of the previous process. In this way, the controller 68controls the flow rate of water and the pressure within the evaporationchamber 71 a according to the heat input to thereby adjust thetemperature of the electrostatic chuck 40 and control the temperature ofthe wafer W to a desired temperature.

Note that if the temperature T of the mounting table 12 is desirablyincreased, the pressure P within the evaporation chamber 71 a may beincreased. On the other hand, if the temperature T of the mounting table12 is desirably decreased, the pressure P within the evaporation chamber71 a may be decreased. For example, in the case where the temperature Tof the mounting table 12 is desirably increased, the controller 68 maycontrol the pressure P within the evaporation chamber 71 a to pressurePA′, which is higher than pressure PA, so that the temperature T of themounting table 12 may be raised to temperature T′. However, normally,the temperature T of the mounting table 12 is preferably not changedduring a process. Thus, the controller 68 controls the pressure P withinthe evaporation chamber 71 a to pressure PA, which is lower thanpressure PA′.

Note that a heater (not shown) is embedded within the mounting table 12.The temperature control apparatus 70 of the present embodiment isconfigured to cool the electrostatic chuck 40, and the heater isconfigured to heat the electrostatic chuck 40. The controller 68controls the cooling operation of the temperature control apparatus 70and the heating operation of the heater to thereby adjust thetemperature of the wafer W placed on the mounting table 12.

As described above, by using the temperature control apparatus 70 of thepresent embodiment, the cooling capacity may be changed by controllingthe flow rate of water. Also, the temperature at which the water is tobe vaporized may be changed by controlling the pressure within theevaporation chamber 71 a. Note that there may be cases in which the heatexchanger 71 is required to vaporize water at a temperature that islower than room temperature such as 0° C. or 5° C. For example, in thecase where water is desirably vaporized within the evaporation chamber71 a that is controlled to approximately 5° C., the controller 68controls the position of the airflow adjustment valve 77 to adjust theflow rate of air and reduce the pressure within the evaporation chamber71 a to approximately several Torr. In the case where water is desirablyvaporized within the evaporation chamber 71 a that is controlled toapproximately 50° C., the controller 68 controls the position of theairflow adjustment valve 77 so that the pressure within the evaporationchamber 71 a may be higher than the pressure when the evaporationchamber 71 a is controlled to 5° C.

As can be appreciated, the temperature control apparatus 70 of thepresent embodiment enables responsive and accurate temperature controlwhile addressing issues of global warming by refraining from using ozonedepleting substances in the refrigerant.

(Temperature Control Example)

In the following, an exemplary temperature control method using thetemperature control apparatus 70 of the present embodiment is describedwith reference to the flowchart of FIG. 6. In the present temperaturecontrol example, the flow rate of water is controlled to be at itsmaximum so that the cooling capacity of the temperature controlapparatus 70 may be maximized and a refrigeration cycle with a highcooling capacity may be achieved.

When the temperature control process of the present example is started,the controller 68 determines whether plasma has been turned ON (stepS62). Upon determining that the plasma has been turned ON, thecontroller 68 starts the operation of the rotary pump 73 and circulateswater at a predetermined flow rate according to the heat input fromplasma (step S64), and controls the valve 76 to be in a fully openposition (step S66).

By controlling the valve 76 to be in the fully open position and therebymaximizing the conductance of the suction pipe 72, the rotary pump 73may be used at its maximum potential. In this way, the water circulatedwithin the refrigeration cycle may always be circulated at a flow ratethat can achieve the desired cooling capacity.

On the other hand, in the present temperature control example, thecontroller 68 controls the flow rate of air introduced into theevaporation chamber 71 a upon adjusting the pressure within theevaporation chamber 71 a such that the temperature of the evaporationchamber 71 a may be controlled to the desired temperature. That is, inthe present temperature control example, the airflow adjustment valve 77is used instead of the valve 76 to adjust the pressure within theevaporation chamber 71 a. Thus, the controller 68 feedback controls theposition of the airflow adjustment valve 77 so that the pressure withinthe evaporation chamber 71 a comes closer to a predetermined pressurelevel for achieving the desired temperature within the evaporationchamber 71 a (step S68).

In this way, the pressure within the evaporation chamber 71 a may alwaysbe controlled to be close to a target value, and the temperature withinthe evaporation chamber 71 a may be accurately controlled.

Then, the controller 68 determines whether the plasma has been turnedOFF (step S70). The controller 68 repeats the processes of steps S64,S66, S68, and S70 until the plasma is turned OFF. Upon determining thatthe plasma has been turned OFF, the controller 68 terminates theoperation of the rotary pump 73 and the circulation of water (step S72),and controls the valve 76 to be in a completely closed position (stepS74).

As described above, in the present temperature control example, thevalve 76 arranged between the heat exchanger 71 and the rotary pump 73is controlled to be completely closed as soon as the plasma is turnedOFF. In this way, the evaporation chamber 71 a may be sealed andprevented from communicating with the vacuum space (reduced-pressurespace) of the rotary pump 73. Because the evaporation chamber 71 aalways communicates with the atmosphere, the pressure within theevaporation chamber 71 a promptly increases to atmospheric pressure oncethe valve 76 is completely closed. As a result, evaporation of water isterminated and the cooling operation is promptly stopped.

By implementing the temperature control method of the presenttemperature control example in the plasma processing apparatus 1 usingthe temperature control apparatus 70 of the present embodiment, ON/OFFoperations of a dynamic cooling operation may be controlled using thevalve 76 arranged between the heat exchanger 71 and the rotary pump 73.That is, the cooling operation may be promptly started by fully openingthe valve 76 as soon as application of a high frequency power from thehigh frequency power supply 32 corresponding to the heat input source isstarted, and the cooling operation may be terminated by completelyclosing the valve 76 as soon as the heat input from the heat inputsource ceases. In this way, temperature responsiveness may be furtherimproved, for example. Also, by controlling the valve 76 in the mannerdescribed above, the cooling capacity of the rotary pump 73 may bemaximized.

Second Embodiment

In the following, a second embodiment of the present invention isdescribed with reference to FIG. 7. The temperature control apparatus 70according to the second embodiment includes a heating cycle in additionto the refrigeration cycle as described above. In the temperaturecontrol apparatus 70 according to the second embodiment, therefrigeration cycle and the heating cycle may be interchangeablyoperated by using switch valves.

The refrigeration cycle is configured by a tubular path including theheat exchanger 71, the suction pipe 72, the rotary pump 73, the oilwater separator 74, a water pipe 81, and the water pipe 75.

The heating cycle is configured by a tubular path including the heatexchanger 71, a water pipe 83, a water pipe 84, a boiler 80, a waterpipe 82, and the water pipe 75.

As can be appreciated, the temperature control apparatus 70 according tothe present embodiment includes a circulation path for the refrigerationcycle that is configured to have the water separated from oil by the oilwater separator 74 circulated back to the heat exchanger 71 via thewater pipe 81, and a circulation path for the heating cycle that isconfigured to have the water introduced into the boiler 80 via the waterpipe 84. Also, the temperature control apparatus 70 according to thepresent embodiment has switch valves V1-V7 arranged at the water pipes75, 81, 82, 83, and 84.

In the case of using the heating cycle, the heat exchanger 71 has toprompt heat exchange that involves condensation of heated vapor and thetransfer of latent heat given up by the vapor. Accordingly, in thepresent embodiment, the boiler 80 is added to generate the heated vapor.The boiler 80 may use heat from a built-in heater 80 a to heat water andgenerate heated vapor, for example. As with the cooling capacity of therefrigeration cycle, data relating to the amount of heat (kW) that maybe output when a given amount of vapor (kg) is converted back to wateris stored in the storage unit of the controller 68, and the controller68 controls the amount of heated vapor to be generated at the boiler 80based on such data. The heating capacity of the heating cycle may bedetermined by the amount of heated vapor generated.

In the present embodiment, the controller 68 performs feedback controloperations based on the detection result of the temperature sensor sothat the current temperature may be close to the target temperature. Thefeedback control operations may be performed using both therefrigeration cycle and the heating cycle by switching between therefrigeration cycle and the heating cycle. In this way, accuratetemperature control may be enabled using a single temperature controlapparatus 70.

For example, in a case where the temperature of the mounting table 12 isdesirably controlled to 25° C., first, the controller 68 operates therefrigeration cycle according to the heat input from plasma. FIG. 8illustrates an operating state of the temperature control apparatus 70during operation of the refrigeration cycle. When the refrigerationcycle is operated, the switch valves V1, V4, and V6 arranged at thecirculation path of the refrigeration cycle are open, and the switchvalves V2, V3, V5, and V7 arranged at the circulation path of theheating cycle are closed. Also, the positions of the valve 76 and theairflow adjustment valve 77 maybe adjusted by the controller 68.

In this case, the water output from the oil water separator 74 passesthrough the water pipe 81 to circulate through the heat exchanger 71where the water is converted into water vapor. The water vapor thenflows into the rotary pump 73 to be dissolved into the oil within therotary pump 73. The mixture of oil and water is then transported to theoil water separator 74 where the oil and water are separated from eachother once again. While the water is circulated in this manner,vaporization heat is removed from the surroundings of the heat exchanger71 when water is turned into water vapor at the heat exchanger 71, andas a result, the surrounding air is cooled as illustrated in FIG. 9. Inthis way, a cooling effect is achieved.

On the other hand, in a case where the temperature of the mounting table12 decreases to a value less than 25° C., the controller 68 operates theheating cycle and performs feedback control operations to adjust thetemperature of the mounting table to 25° C. FIG. 10 illustrates anoperating state of the temperature control apparatus 70 during operationof the heating cycle. When the heating, cycle is operated, the switchvalves V2, V3, V5, and V7 arranged at the circulation path of theheating cycle are open, and the switch valves V1, V4, and V6 arranged atthe circulation path of the refrigeration cycle are closed. Also, thevalve 76 is closed in this case but the position of the airflowadjustment valve 77 may be adjusted by the controller 68.

In this case, water output from the oil water separator 74 passesthrough the water pipe 84 and enters the boiler 80. The water is heatedby the heater 80 a at the boiler 80 and heated vapor is generated as aresult. The generated heated vapor passes through the water pipes 82 and75 and circulates through the heat exchanger 71 where the heated vaporis converted back to water. The water within the heat exchanger 71 thenenters the water pipe 83 and is transported back to the boiler 80 viathe water pipe 84. While the water is circulated in this manner, asillustrated in FIG. 11, condensation heat is given up and transferred tothe surroundings of the heat exchanger 71 when the water vapor is turnedinto water at the heat exchanger 71, and as a result, the surroundingair is heated. In this way, a heating effect is achieved.

In the temperature control apparatus 70 according to the presentembodiment, when the temperature of the mounting table 12 is raised toohigh by the heating cycle, the controller 68 switches the positions ofthe switch valves V1-V7 to operate the refrigeration cycle. On the otherhand, when the temperature of the mounting table 12 becomes too low, thecontroller 68 switches the positions of the switch valves V1-V7 tooperate the heating cycle and performs feedback control operations sothat the temperature of the mounting table 12 may be controlled to thedesired temperature of 25° C., for example. By repeating the operationsas described above, hot air may be cooled during operation of therefrigeration cycle, and cool air may be heated during operation of theheating cycle as illustrated in FIG. 12. In this way, accuratetemperature control may be performed using a single temperature controlapparatus 70.

Note that during operation of the heating cycle, the interior of theevaporation chamber 71 a is under increased pressure. For example,during operation of the heating cycle, the evaporation chamber 71 a maybe under a pressure of 0.2 MPa. On the other hand, during operation ofthe refrigeration cycle, the interior of the evaporation chamber 71 amay be under a reduced pressure of 0.001 MPa, for example. Also, in thepresent embodiment, the pressure within the evaporation chamber 71 a maybe controlled to an increased-pressure or a reduced-pressure byadjusting at least one of the rotation speed of the rotor 73 a, theposition of the valve 76, and the position of the airflow adjustmentvalve 77.

According to an aspect of the present invention, the temperature controlapparatus 70 according to the embodiments described above may performtemperature control without using an ozone depleting substance in therefrigerant. That is, the temperature control apparatus 70 according toembodiments of the present invention may be effectively used as acountermeasure against global warming. According to another aspect ofthe present invention, a refrigeration cycle and a heating cycle may beimplemented within a closed circuit so that the temperature controlapparatus 70 may be used in accordance with a current usage environment.In this way, system development costs may be reduced and introduction ofthe system may be facilitated, for example.

Also, in the temperature control apparatus 70 according to embodimentsof the present invention, the pressure within the heat exchanger 71 doesnot have to be controlled to a high pressure. In fact, the pressurewithin the heat exchanger 71 is controlled to a reduced-pressure inorder to enable vaporization of a liquid under a temperature of lessthan 100° C. Accordingly, in a case where the temperature controlapparatus 70 is installed in a plasma processing apparatus, apredetermined portion of the temperature control apparatus 70 may beeasily controlled to a reduced pressure in view of the fact thatcontrolling the interior of a chamber to a reduced-pressure atmosphereis normally performed at the plasma processing apparatus. Also, achamber with a relatively small heat capacity may be used in the heatexchanger 71 so that temperature responsiveness may be improved andenergy resources may be conserved, for example.

<Concluding Remarks>

Although the present invention has been described above with respect tocertain illustrative embodiments, the present invention is not limitedto these embodiments. That is, numerous variations and modificationswill readily occur to those skilled in the art, and the presentinvention includes all such variations and modifications that may bemade without departing from the scope of the present invention. Also,embodiments and modifications of the present invention may be combinedto the extent practicable.

For example, according to an aspect of the present invention, a plasmaprocessing apparatus may be provided that includes a processing chamberin which a plasma process is performed; a gas supply source configuredto supply gas to the processing chamber; a plasma source configured tosupply power for plasma generation and generate plasma from gas withinthe processing chamber; a heat exchanger that is arranged in at leastone of the processing chamber, a mounting table arranged in theprocessing chamber, an upper electrode arranged in the processingchamber, and a deposition shield arranged in the processing chamber, andis configured to exchange heat using a phase change of a refrigerant; arotary pump configured to receive the refrigerant from the heatexchanger and fuse the refrigerant with oil contained inside the rotarypump; and an oil refrigerant separator configured to receive therefrigerant fused with the oil from the rotary pump and separate therefrigerant from the oil. The plasma processing apparatus furtherincludes a refrigeration cycle that implements a cooling function bycirculating the refrigerant separated from the oil back to the heatexchanger.

According to another aspect of the present invention, a temperaturecontrol apparatus according to an embodiment of the present invention isnot limited to controlling the temperature of the electrostatic chuck 40of a plasma processing apparatus. For example, a temperature controlapparatus according to an embodiment of the present invention may beconfigured to control at least one of the electrostatic chuck 40, theupper electrode (shower head 38), a deposit shield, and the processingchamber 10 of a plasma processing apparatus and may have the heatexchanger 71 arranged near at least one of the mounting table 12, theupper electrode, the deposition shield, and the processing chamber 10.

According to another aspect of the present invention, a temperaturecontrol apparatus according to an embodiment of the present invention isnot limited to being arranged near one or more of the above members ofthe plasma processing apparatus to cool or heat the above members. Forexample, a temperature control apparatus according to an embodiment ofthe present invention may be used to control the temperature of achiller unit arranged at the plasma processing apparatus.

According to another aspect of the present invention, a processingapparatus that uses a temperature control apparatus according to anembodiment of the present invention is not limited to a plasmaprocessing apparatus. For example, a temperature control apparatusaccording to an embodiment of the present invention may be installed andused in a processing chamber of a refrigerator to prevent thetemperature within the refrigerator from increasing as a result of aheat input from a heat input source. Also, a temperature controlapparatus according to an embodiment of the present invention may beinstalled and used in a processing chamber of an air conditioner.Moreover, a temperature control apparatus according to an embodiment ofthe present invention may be installed in any type of processing chamberto achieve cooling or heating within the processing chamber.

Regardless of the type of processing apparatus, the temperature controlapparatus installed therein may be configured to perform temperaturecontrol as illustrated in FIG. 4 as well as temperature control asillustrated in FIG. 6. That is, the valve 76 arranged at the suctionpipe 72 may be controlled to fully open in conjunction with the start ofoperation of a heat input source, and the valve 76 may be controlled tocompletely close in conjunction with the termination of the operation ofthe heat input source. In this way, the temperature may be dynamicallycontrolled, for example.

Also, note that in the case where the temperature control apparatusaccording to an embodiment of the present invention is installed in aplasma processing apparatus, the type of plasma processing apparatus isnot limited to a parallel-plate type etching apparatus but may also beapplied to a cylindrical RLSA (radical line slot antenna) plasmaprocessing apparatus, an ICP (inductively coupled plasma) plasmaprocessing apparatus, a microwave plasma processing apparatus, or someother type of plasma processing apparatus. Also, the type of processperformed in the plasma processing apparatus is not limited to etching,but may include other processes such as film formation, ashing, andsputtering, for example.

The present application is based on and claims the benefit of priorityof Japanese Patent Application No. 2011-249081 filed on Nov. 14, 2011,and U.S. Provisional Application No. 61/568181 filed on Dec. 8, 2011,the entire contents of which are herein incorporated by reference.

DESCRIPTION OF THE REFERENCE NUMERALS

1 plasma processing apparatus

10 processing chamber

12 mounting table (lower electrode)

32 high frequency power supply

38 shower head (upper electrode)

40 electrostatic chuck

62 gas supply source

68 controller

70 temperature control apparatus

71 heat exchanger

72 suction pipe

71 a evaporation chamber

73 rotary pump

73 a rotor

74 oil water separator

75 water pipe

76 valve

77 airflow adjustment valve

80 boiler

V1-V7 switch valve

1. A temperature control apparatus comprising: a heat exchangerconfigured to exchange heat using a phase change of a refrigerant; arotary pump configured to receive the refrigerant from the heatexchanger and fuse the refrigerant with oil contained inside the rotarypump; an oil refrigerant separator configured to receive the refrigerantfused with the oil from the rotary pump and separate the refrigerantfrom the oil; and a refrigeration cycle that implements a coolingfunction by circulating the refrigerant separated from the oil back tothe heat exchanger.
 2. The temperature control apparatus as claimed inclaim 1, wherein the rotary pump reduces a pressure within anevaporation chamber arranged in the heat exchanger by rotating a rotorof the rotary pump; and the heat exchanger performs cooling by absorbingvaporization heat upon vaporizing the refrigerant within the evaporationchamber under the reduced pressure.
 3. The temperature control apparatusas claimed in claim 1, wherein the refrigerant separated from the oil bythe oil refrigerant separator circulates through the heat exchanger, therotary pump, and the oil refrigerant separator; and the oil separatedfrom the refrigerant by the oil refrigerant separator is recovered bythe rotary pump.
 4. The temperature control apparatus as claimed inclaim 1, further comprising: a boiler configured to heat therefrigerant; and a heating cycle that implements a heating function bycirculating the heated refrigerant through the heat exchanger and theboiler; wherein the heat exchanger receives the heated refrigerant fromthe boiler and performs heating by releasing condensation heat uponliquefying the heated refrigerant within the evaporation chamber.
 5. Thetemperature control apparatus as claimed in claim 4, further comprising:a switch valve for switching between the refrigeration cycle and theheating cycle.
 6. The temperature control apparatus as claimed in claim5, wherein the refrigerant separated by the oil refrigerant separatorcorresponds to water that is circulated through the refrigeration cycleor the heating cycle in response to a switching of the switch valve. 7.The temperature control apparatus as claimed in claim 1, wherein theheat exchanger is arranged in at least one of a processing chamber of aplasma processing apparatus in which a plasma process is performed, amounting table arranged in the plasma processing apparatus, an upperelectrode arranged in the plasma processing apparatus, and a depositionshield arranged in the plasma processing apparatus.
 8. A processingapparatus comprising: a temperature control apparatus that is mounted toa temperature control object and is configured to control a temperatureof the temperature control object, the temperature control apparatusincluding a heat exchanger configured to exchange heat using a phasechange of a refrigerant; a rotary pump configured to receive therefrigerant from the heat exchanger and fuse the refrigerant with oilcontained inside the rotary pump; an oil refrigerant separatorconfigured to receive the refrigerant fused with the oil from the rotarypump and separate the refrigerant from the oil; and a refrigerationcycle that implements a cooling function by circulating the refrigerantseparated from the oil back to the heat exchanger.
 9. A temperaturecontrol method that is implemented by a temperature control apparatusincluding a heat exchanger configured to exchange heat using a phasechange of a refrigerant, a rotary pump configured to receive therefrigerant from the heat exchanger and fuse the refrigerant with oilcontained inside the rotary pump, and an oil refrigerant separatorconfigured to receive the refrigerant fused with the oil from the rotarypump and separate the refrigerant from the oil, the temperature controlmethod comprising the steps of: circulating the refrigerant separatedfrom the oil back to the heat exchanger; and adjusting at least one of arotation speed of a rotor of the rotary pump, a position of a valvearranged at a connecting portion of the rotary pump and the heatexchanger, and a position of an airflow adjustment valve arranged at aconnecting portion of the oil refrigerant separator and the heatexchanger.
 10. The temperature control method as claimed in claim 9,further comprising the step of: controlling a start of a coolingoperation and an end of the cooling operation by controlling the valveto fully open in conjunction with a start of an operation of a heatinput source and controlling the valve to completely close inconjunction with a termination of the operation of the heat inputsource.
 11. The temperature control method as claimed in claim 9,further comprising the step of: adjusting a pressure within anevaporation chamber arranged in the heat exchanger by controlling theposition of the airflow adjustment valve.
 12. The temperature controlmethod as claimed in claim 10, wherein the heat input source correspondsto a plasma source that is used in a plasma processing apparatus.